Wall thickness estimation based on modelling nonstationary heat transfer in a glass furnace

dc.bibliographicCitation.firstPage25
dc.bibliographicCitation.journalTitleGlass Science and Technologyeng
dc.bibliographicCitation.lastPage30
dc.bibliographicCitation.volume77
dc.contributor.authorVráble, Peter
dc.contributor.authorŠimurka, Peter
dc.contributor.authorLiška, Marek
dc.date.accessioned2024-01-05T14:05:48Z
dc.date.available2024-01-05T14:05:48Z
dc.date.issued2004
dc.description.abstractFurnaces in the glass industry suffer from refractory corrosion at specific positions. Knowledge of wall thickness of a furnace at the metal line is necessary information for a proper start of external cooling in order to prevent complete corrosion of refractory. An application of a noninvasive method for residual wall thickness estimation is presented in this paper. Combination of modelling and experimental surface temperature record of a nonstationary heat transfer is necessary in order to calculate the actual wall thickness. A formula was derived for a temperature dependent effective heat transfer coefficient needed for calculation. Sensitivity analysis proved that the method is robust enough to get reliable results. The approach used was an example of reasonable exploitation of modelling in the glass industry.eng
dc.description.versionpublishedVersion
dc.identifier.urihttps://oa.tib.eu/renate/handle/123456789/13920
dc.identifier.urihttps://doi.org/10.34657/12950
dc.language.isoeng
dc.publisherOffenbach : Verlag der Deutschen Glastechnischen Gesellschaft
dc.relation.issn0946-7475
dc.rights.licenseCC BY 3.0 DE
dc.rights.urihttps://creativecommons.org/licenses/by/3.0/de/
dc.subject.ddc660
dc.titleWall thickness estimation based on modelling nonstationary heat transfer in a glass furnaceeng
dc.typeArticleeng
dc.typeTexteng
tib.accessRightsopenAccess
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